C           *** CONTRL0L DATA ***
C
C   THIS SECOND EXAMPLE USES THE SAME NETWORK BUT ASSUMED TO BE AN OPEN LOOP.
C   FIXFLO ANALYSIS EMPLOYED. NO ADJUST SUBROUTINE
2117.
FIXFLO
GAS
END
C           *** NETWORK DATA ***
C
C   NETWORK ELEMENTS ARE THE SAME AS THE FIRST EXAMPLE'S
5,1,2,.1,.01,-1.7,.1536,110.
10,2,11,.1,.00217,-1.66557,14.12,110.
15,2,11,.1,.00217,-1.66557,14.12,110.
20,2,3,.1,.01,-1.48,206.3,110.
25,3,11,.1,.003,-2.,2.367,110.
30,2,4,.1,.01,-1.48,206.3,110.
35,4,11,.1,.003,-2.,2.367,110.
40,2,5,.1,.01,-1.84,12.89,110.
45,5,11,.1,.0074,-2.,2.367,110.
50,2,6,.1,.0225,-1.384,160.,110.
55,6,11,.179,.175,1.01,3.,110.
60,2,7,.1,.0313,-1.464,156.,110.
65,7,6,.179,.175,1.01,1.5,110.
70,2,8,.1,.0225,-1.384,160.,110.
75,8,7,.179,.175,1.01,2.,110.
80,2,9,.1,.0313,-1.464,156.,110.
85,9,10,.1083,.157,.441,.5,110.
90,10,8,.1083,.157,.441,.01,110.
95,11,12,.1,.01,-1.83,.2655,110.
END
C           *** INITIAL DATA ***
C
C   ALSO SAME INITIAL PRESSURE DATA
1,0.
2,-1.
3,-2.
4,-2.
5,-2.
6,-7.6
7,-6.9
8,-6.0
9,-2.
10,-3.
11,-8.2
12,-100.
END
C           *** BOUNDARY DATA ***
C
C   NO BOUNDARY
END
C           *** CURVE DATA ***
C
C   IN FIXFLO ANALYSIS, A KNOWN TOTAL FLOW RATE IS ENTERED INSTEAD OF A PUMP
C   CURVE. THIS EXAMPLE USES THE FLOW RATE THE SAME AS FIRST EXAMPLE'S TOTAL
C   FLOW
C
C   BELOW ARE FIXFLO INLET  AND OUTLET NODE ID'S WITH 890. LB/HR CONST. FLOWRATE
1,12,890.
C   PROPERTIES OF AIR AT 2117. PSF  (14.7 PSI). 7 POINTS ARE ENTERED
 7 2117.  0.0,.08629,.03939  20.,.08269,.04075  40.0,.07938,.04208
          60.,.07633,.04339  80.,.07350,.04467  100.,.07087,.04594
         120.,.06843,.04718
END
C   THE FOLLOWING FOUR LINE ELEMENTS ARE TO BE OUTPUT
4.,5,25,35,45
END
